EP0016690A1 - Vorrichtung zur Abscheidung fester Suspensionsteilchen in einem Flüssigkeitsstrom - Google Patents

Vorrichtung zur Abscheidung fester Suspensionsteilchen in einem Flüssigkeitsstrom Download PDF

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Publication number
EP0016690A1
EP0016690A1 EP80400334A EP80400334A EP0016690A1 EP 0016690 A1 EP0016690 A1 EP 0016690A1 EP 80400334 A EP80400334 A EP 80400334A EP 80400334 A EP80400334 A EP 80400334A EP 0016690 A1 EP0016690 A1 EP 0016690A1
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EP
European Patent Office
Prior art keywords
influent
compartment
mixing
solids
settling
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP80400334A
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English (en)
French (fr)
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EP0016690B1 (de
Inventor
Kamlesh Kumar Jain
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fram Industrial Filter Corp
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Fram Industrial Filter Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Fram Industrial Filter Corp filed Critical Fram Industrial Filter Corp
Publication of EP0016690A1 publication Critical patent/EP0016690A1/de
Application granted granted Critical
Publication of EP0016690B1 publication Critical patent/EP0016690B1/de
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281—Installations for water purification using chemical agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/01—Separation of suspended solid particles from liquids by sedimentation using flocculating agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2405—Feed mechanisms for settling tanks
    • B01D21/2416—Liquid distributors with a plurality of feed points

Definitions

  • the present invention relates to a process for separating solids from suspensions in a liquid influent, as well as an apparatus for par- forming this process. More specifically, the invention pertains to a waste treatment system for separating particulate matters from an influent carrier, and more particularly pertains to a system with a perforated plate for main- taming widely different hydrodynamic conditions in specific compartments of a separator assembly.
  • Tnus it is an object of this invention to provide a waste treatment assembly and process for controlling and directing convective momentum to maintain widely different hydrodynamic conditions in specific compartments of the assembly, by which the efficiency of the assembly and process are improved and the rate of settlementation of the suspensions is increased.
  • the influent will advantageously be stirred while flowing through the mixing chamber, said stirring being sequentially performed with a fast mixing speed to insure mixing of additives with the influent suspensions and with a slower mixing speed to promote agglomeration of microflocs, which enables suspensions to be directed through the various flow paths with a minimum amount of solids breakup.
  • An apparatus for practising the above-defined process will advantageously comprise an inner mixing compartment and an outer settling compartment formed in a separator unit, said compartments communicating with each other through hydrodynamic changing means which are so designed as to transfer the influent from the mixing compartment into the settling compartment while reducing momentum transfer to the liquid in said settling compartment and thus increasing the rate of sedimentation of the solids suspended in the liquid, and said hydrodynamic changing means will then comprise a perforated plate, the perforations of which are inclined with respect to the direction of transfer as well as relatively to each other so as to provide the various flows of liquid exiting same with tangential velocity components which tend to cancel one another.
  • some of the perforations in the plate will be inclined symmetrically to the other ones with respect to a plane normal to the plane of said plate. More specifically, these perforations will be inclined by an angle of about 60° with respect to the plane of the plate.
  • a stirring paddle which is driven by motor means sequentially providing same with a fast mixing speed to insure mixing of additives with the influent suspensions, and with a slower mixing speed to promote agglomeration of microflocs.
  • An improved, packaged, waste treatment separator assembly is fundamentally a single or unit separator assembly for separating suspensions, particles, solids, grease, etc. from a liquid influent carrier.
  • Assembly 1 may be divided for explanation purposes into the following three basic compartments, or sections : inner mixing compartment 3, perforated plate 5, and outer settling compartment 7.
  • Assembly 1 is manufactured from prior art materials typically utilized in the art of constructing separator units for waste treatment systems.
  • the size of assembly 1 is principally determined by the specific type of waste treatment applications assembly 1 is designed to be employed in.
  • assembly 1 may be of a variety of sizes. In a typical embodiment, assembly 1 can be approximately 400 millimeters high and can have a diameter of approximately 220 mm for a flow rate of approximately 300 cc per minute. These dimensions of course will vary depending on the flow rate of the stream to be treated.
  • Inner mixing compartment 3 is structured so as to have an increasing area and volume configuration as shown in Figures 1 and 4 or any other configuration that is structured to possess increasing area and volume.
  • the increasing area and volume configuration of mixing compartment 3 helps in controlling the rate of mixing as the stream moves downwards within the confines of compartment 3.
  • Compartment 3 is centrally located within an upper area or zone 11 of outer settling compartment 7 and is connected thereto by conventional attachment methods.
  • the diameter of compartment 3 at or near its top and also at its base is not fixed, and is in essence determined by many variables, such as : the kind of waste that is processed, the input velocity of the influent, and the desired rate of settlementation. In the previous example given for assembly 1, compartment 3 will have a base diameter of approximately 127 mm, a height of approximately 203 mm, and an upper diameter of approximately 25 mm.
  • Compartment 3 includes an agitator subassembly, generally designated as 12, for mixing chemical additives, such as commercially available flocculants, with the influent.
  • Agitator 12 further functions to promote agglomeration and coagulation of solids in the influent.
  • Agitator 12 comprises a stirrer paddle 17, shaft 15 and a motor subassembly.
  • the motor is not here illustrated, it is also of a kind normally employed in the waste treatment mixing tanks.
  • Shaft 15 extends centrally downwards into inner compartment 3 and has the motor connected at its upper end typically outside of assembly 1.
  • Stirrer 17 is connected at the lower end of shaft 15 through which stirrer 17 is driven at both high and low speeds.
  • Stirrer 17 extends to a depth within mixing compartment 3 that is sufficient to insure a thorough mixing of the chemicals and influent, and to promote flocculation, aggregation, or agglomeration of solids therein.
  • the size of stirrer 17 is also a function of variables similar to those variables enumerated while discussing the size of assembly 1 and compartment 3. In the previous example given for assembly 1, stirrer 17 moves within a circular area having approximately a 76 mm diameter and 25 mm in height.
  • agitator 12 further includes a conventional scraper unit 19.
  • Scraper unit 19 is attached to the lower end of shaft 15 below stirrer 17.
  • Scraper 19 operates to prevent the hampering of influent flowing from inner mixing compartment 3 to settling compartment 7 by controlling or monitoring the amount or accumulation of sedimentation build up on perforated plate 5.
  • Perforated plate 5 forms the base of mixing compartment 3 and also separates the inner mixing compartment 3 from the outer settling compartment, or said differently, plate 5 connects the two compartments 3 and 7 to each other. Additionally, perforated plate 5 acts to maintain widely different hydrodynamic conditions in compartments 3 and 7.
  • Plate 5 generally has a disc configuration with an outer diameter large enough to fit the inner base diameter of compartment 3. Plate 5, as best illustrated in Figures 2 and 3, includes a plurality of spaced flow paths or holes 21 therein.
  • Flow paths 21 operate to direct and transport influent into compartment 7 from compartment 3.
  • flow paths 21 will have a diameter of 12,5 mm.
  • Flow paths 21 are orientated or inclined within plate 5, so that tangential velocity components of convective momentum (which momentum is associated with flowing currents of influent) are cancelled and/or minimized.
  • a first certain number of paths 21 are orientated within plate 5 to form an angle in inclination of around 60° with respect to second or other certain remaining paths 21, and with respect to a horizontal reference position.
  • the reference position is established by the base of plate 5 or compartment 3.
  • FIG. 3 An alternate embodiment of plate 5 is shown in Figure 3, wherein flow paths 21 are tapered so that the influent flows through a larger opening when it exits the plate than when it enters the plate. This results in reducing the momentum of the influent as it enters the lower section of outer compartment 7.
  • Outer compartment 7 includes a base area 23 wherein settled suspension or sludge is accumulated for withdrawal.
  • Base area 23 is a flat circular area having an outlet for accumulating settled solids and having an outlet port 25 from which sludge is withdrawn.
  • An annulus 27 is formed in the area between outer wall 29 of inner compartment 3 and inner wall 31 of compartment 7. In the upper most reaches or areas of compartment 7, a second outward port 33 is positioned to enable removal of clarified liquids, grease, etc.
  • base area 23 is a-conical shaped sludge collector 35, as depicted in Figure 4. Additionally, the length of shaft 15 is extended so that a non annular blade shaped scraper plow 37 is attached thereto.
  • Conical sludge. compartment 35 operates to improve the rate of settlementation by providing additional surface on which small particles not yet settled in outer settling compartment 7 can be caused to settle, and by isolating settled solids in sludge compartment 35 from the flowing currents of the influent.
  • influent is first fed into port 38.
  • Chemical coagulant and/or flocculant additives are mixed with the influent either before the influent enters assembly 1 or just as the influent enters inner compartment 3.
  • the influent and the additives are mixed by paddle 17.
  • the mixing speed of paddle 17 is controlled so that mixing is accomplished in two stages.
  • the influent and additives are rapidly mixed to create high turbulence thereby insuring a thorough mixing of the influent and additives.
  • the influent and additives are slowly mixed to create tangential velocity components of sufficient magnitude to cause and promote agglomeration of solids, including the microflocs.
  • Scraper unit 19 seen in Figure 4, when applicable, stirs and aids accumulated suspensions that have settled on plate 5'to enter flow paths 21 and pass through to compartment 7.
  • compartment 3 causes momentum to be continuously decreased by slowing current flaw as influent moves downwards in compartment 3, from which the magnitude of the tangential and axial components of veioci- ty are decreased. Hence, coagulated and flocculated solids are made to settle out of the influent towards plate 5.
  • plate 5 As earlier mentioned, functions to maintain widely different hydrodynamic conditions in compartments 3 and 7, and also functions to isolate settling suspensions within compartment 7 from currents that tend to disintegrate the suspensions. And as described above, tangential components of velocity associated with the streams of currents leaving compartment 3 via paths 21 of the plate 5 nullify one another. Furthermore, by using a single packaged unit, abrupt variations in momentum and velocities are avoided during the transfer of a suspension that would tend to break up agglomerated solids.
  • the rate of sedimentation in compartment 7 is improved because the settling solids transferred thereto have only downward velocity and momentum while settling.
  • the possibility of disturbing solids that have settled out in compartment 7 with high input momentum of flowing currents fed into port 38 are eliminated by confining it to compartment 3.
  • the rate of concentration of accumulated sludge is also improved, the reason for this is that the possibility of disturbing accumulated solids with the input momentum of entering influent is eliminated or at least significantly minimized.
  • plow 37 removes or directs settled sludge to collector 35.
  • Interior wall 41 of conically configured sludge collector 35 provides additional area for accumulating settled sludge.
  • collector 35 tends to isolate the settled sludge from current flow and momentum. As a consequence of collector 35, in conjunction with the effect that walls 41 have on settling solids, the ability to concentrate collected sludge is improved.
  • assembly 1 includes the following incomplete list of advantageous characteristics : the functions of particle agglomeration, solid sedimentation are combined in a single unit. When compared to conventional separators, a reduction by 30 to 50 percent in the total process time for separating solids from liquids is possible. An improved quality and amount of clarified liquid effluent is able to be withdrawn in a shorter time than heretofore acquired with prior art separators. An increase in hydrodynamic stability characteristics for a continuous sedimentation process is possible. Convective momentum is continuously decreased and minimized during all process cycles or stages of separating. The ability to maintain widely different hydrodynamic conditions in inner and outer compartments 3 and 7 is now possible. Abrupt variations in velocity which tend to break up aggregated flocs during transference of a flocculated stream are avoided. Convective momentum that disrupts settled sludge is minimized, and settled sludge is isolated from the momentum of influent currents.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Physical Water Treatments (AREA)
EP80400334A 1979-03-16 1980-03-14 Vorrichtung zur Abscheidung fester Suspensionsteilchen in einem Flüssigkeitsstrom Expired EP0016690B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/021,276 US4224157A (en) 1979-03-16 1979-03-16 Process and apparatus for separating solids from suspensions of influent
US21276 1987-03-03

Publications (2)

Publication Number Publication Date
EP0016690A1 true EP0016690A1 (de) 1980-10-01
EP0016690B1 EP0016690B1 (de) 1983-02-16

Family

ID=21803310

Family Applications (1)

Application Number Title Priority Date Filing Date
EP80400334A Expired EP0016690B1 (de) 1979-03-16 1980-03-14 Vorrichtung zur Abscheidung fester Suspensionsteilchen in einem Flüssigkeitsstrom

Country Status (10)

Country Link
US (1) US4224157A (de)
EP (1) EP0016690B1 (de)
JP (1) JPS55124508A (de)
AU (1) AU536195B2 (de)
BR (1) BR8001589A (de)
CA (1) CA1144110A (de)
DE (1) DE3061966D1 (de)
ES (1) ES8100112A1 (de)
NO (1) NO152969C (de)
ZA (1) ZA801146B (de)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2568564A1 (fr) * 1984-07-31 1986-02-07 Alsthom Atlantique Procede de clarification a lit de boue pour liquide charge de matieres solides
CN106807132A (zh) * 2017-02-15 2017-06-09 安庆师范大学 一种用于污水处理的透水槽

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989005685A1 (en) * 1987-12-18 1989-06-29 Houston Winn Fuel filter and separator
DE4134388C2 (de) * 1991-10-17 1994-09-22 Felder Anton Vorrichtung und Verfahren zur zentrischen Beschickung von Rundbecken durch Abwasser
US5453187A (en) * 1994-02-15 1995-09-26 Plumb; Arnold D. Food, oil and grease accumulation apparatus and method
US5480540A (en) * 1994-10-17 1996-01-02 General Electric Company Spray apparatus for separating solids from fluids
US5597477A (en) * 1995-05-11 1997-01-28 Harry, Iii; David W. Sewage effluent disposal system having sparger in holding tank
CN1314502A (zh) * 2000-03-21 2001-09-26 亚洲电镀器材有限公司 混合设备
US20040149639A1 (en) * 2002-11-15 2004-08-05 Weston Vaughn J. Apparatus for mixing and dispensing influent slurry into a tank and systems incorporating same
JP4254426B2 (ja) * 2003-08-27 2009-04-15 栗田工業株式会社 沈殿槽装置
CA2857888C (en) * 2013-07-29 2018-03-20 Calx Limited Apparatus and method for treating slurries
US9676642B2 (en) 2014-10-01 2017-06-13 ClearCove Systems, Inc. Method for selectively treating sludge to remove components therefrom
US10308538B2 (en) 2014-10-01 2019-06-04 ClearCove Systems, Inc. Apparatus for separating materials from an influent stream
US9586845B2 (en) 2014-10-01 2017-03-07 ClearCove Systems, Inc. Method and apparatus for separating biologically digestible materials from an influent stream
US10308539B2 (en) 2014-10-01 2019-06-04 ClearCove Systems, Inc. Apparatus for treatment of sludge
JP6492981B2 (ja) * 2015-06-02 2019-04-03 王子ホールディングス株式会社 水処理装置および水処理方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2201282A (en) * 1937-01-19 1940-05-21 Arndt Charles Separator
US2275954A (en) * 1939-01-09 1942-03-10 Gibson William Robert Water treatment plant
US2891008A (en) * 1955-08-22 1959-06-16 Hungerford & Terry Inc Water purification coagulation apparatus with perforate plate flow controllers
US3221889A (en) * 1962-06-13 1965-12-07 Hirsch Abraham Adler Effluent removal structure for settling tanks and reservoirs
US3353676A (en) * 1966-05-05 1967-11-21 Hirsch A Adler Radial flow settling tank with complete volumetric transit for water and waste treatment
DE2015529A1 (de) * 1970-04-01 1971-10-21 Maschinenfabrik Ratzinger GmbH, 8000 München Vorrichtung rum Entwässern und Klassieren von Sand, Kies und dergleichen

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2602465A (en) * 1949-10-18 1952-07-08 Otto C Goehring Inlet tube for storage tanks and the like
US3353679A (en) * 1966-01-05 1967-11-21 Hirsch A Adler Triangular-type horizontal flow settling basins
JPS5140053B1 (de) * 1969-12-11 1976-11-01

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2201282A (en) * 1937-01-19 1940-05-21 Arndt Charles Separator
US2275954A (en) * 1939-01-09 1942-03-10 Gibson William Robert Water treatment plant
US2891008A (en) * 1955-08-22 1959-06-16 Hungerford & Terry Inc Water purification coagulation apparatus with perforate plate flow controllers
US3221889A (en) * 1962-06-13 1965-12-07 Hirsch Abraham Adler Effluent removal structure for settling tanks and reservoirs
US3353676A (en) * 1966-05-05 1967-11-21 Hirsch A Adler Radial flow settling tank with complete volumetric transit for water and waste treatment
DE2015529A1 (de) * 1970-04-01 1971-10-21 Maschinenfabrik Ratzinger GmbH, 8000 München Vorrichtung rum Entwässern und Klassieren von Sand, Kies und dergleichen

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2568564A1 (fr) * 1984-07-31 1986-02-07 Alsthom Atlantique Procede de clarification a lit de boue pour liquide charge de matieres solides
EP0174232A1 (de) * 1984-07-31 1986-03-12 Alsthom Verfahren zum Klären einer feststoffbeladenen Flüssigkeit mittels eines Schlammbettes
CN106807132A (zh) * 2017-02-15 2017-06-09 安庆师范大学 一种用于污水处理的透水槽

Also Published As

Publication number Publication date
AU536195B2 (en) 1984-04-19
AU5633880A (en) 1980-09-18
NO152969C (no) 1985-12-27
EP0016690B1 (de) 1983-02-16
ES489566A0 (es) 1980-11-01
JPS55124508A (en) 1980-09-25
DE3061966D1 (en) 1983-03-24
CA1144110A (en) 1983-04-05
ES8100112A1 (es) 1980-11-01
US4224157A (en) 1980-09-23
ZA801146B (en) 1981-03-25
NO800745L (no) 1980-09-17
NO152969B (no) 1985-09-16
BR8001589A (pt) 1980-11-18

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